'Dark' CO2 fixation in succinate fermentations enabled by direct CO2 delivery via hollow fiber membrane carbonation

被引:0
|
作者
Godar, Amanda G. [1 ]
Chase, Timothy [2 ]
Conway, Dalton [2 ]
Ravichandran, Dharneedar [3 ]
Woodson, Isaiah [2 ]
Lai, Yen-Jung [4 ]
Song, Kenan [3 ]
Rittmann, Bruce E. [4 ,5 ]
Wang, Xuan [1 ]
Nielsen, David R. [2 ]
机构
[1] Arizona State Univ, Sch Life Sci, Tempe, AZ USA
[2] Arizona State Univ, Sch Engn Matter Transport & Energy, BDC C499C, Tempe, AZ 85282 USA
[3] Arizona State Univ, Sch Mfg Syst & Networks, Tempe, AZ USA
[4] Arizona State Univ, Biodesign Swette Ctr Environm Biotechnol, Tempe, AZ USA
[5] Arizona State Univ, Sch Sustainable Engn & Built Environm, Tempe, AZ USA
基金
美国国家科学基金会;
关键词
Membrane carbonation; Membrane bioreactor; Succinate fermentation; Dark CO2 fixation; METABOLIC EVOLUTION; CLEANER PRODUCTION; DIOXIDE; MICROALGAE; PHOTOBIOREACTOR; OPTIMIZATION; STRATEGIES; PATHWAYS; STRAINS; GAS;
D O I
10.1007/s00449-023-02957-3
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Anaerobic succinate fermentations can achieve high-titer, high-yield performance while fixing CO2 through the reductive branch of the tricarboxylic acid cycle. To provide the needed CO2, conventional media is supplemented with significant (up to 60 g/L) bicarbonate (HCO3-), and/or carbonate (CO32-) salts. However, producing these salts from CO2 and natural ores is thermodynamically unfavorable and, thus, energetically costly, which reduces the overall sustainability of the process. Here, a series of composite hollow fiber membranes (HFMs) were first fabricated, after which comprehensive CO2 mass transfer measurements were performed under cell-free conditions using a novel, constant-pH method. Lumen pressure and total HFM surface area were found to be linearly correlated with the flux and volumetric rate of CO2 delivery, respectively. Novel HFM bioreactors were then constructed and used to comprehensively investigate the effects of modulating the CO2 delivery rate on succinate fermentations by engineered Escherichia coli. Through appropriate tuning of the design and operating conditions, it was ultimately possible to produce up to 64.5 g/L succinate at a glucose yield of 0.68 g/g; performance approaching that of control fermentations with directly added HCO3-/CO32- salts and on par with prior studies. HFMs were further found to demonstrate a high potential for repeated reuse. Overall, HFM-based CO2 delivery represents a viable alternative to the addition of HCO3-/CO32- salts to succinate fermentations, and likely other 'dark' CO2-fixing fermentations.
引用
收藏
页码:223 / 233
页数:11
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